Methods and systems for spillback control of in-line mixing of hydrocarbon liquids

US12011697B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12011697-B2
Application numberUS-202318219280-A
CountryUS
Kind codeB2
Filing dateJul 7, 2023
Priority dateDec 30, 2019
Publication dateJun 18, 2024
Grant dateJun 18, 2024

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

Methods and systems of admixing hydrocarbon liquids from two or more sets of tanks into a single pipeline to provide in-line mixing thereof. In an embodiment of the in-line mixing system, hydrocarbon liquids stored in at least one tank of each of two or more sets of tanks positioned at a tank farm are blended into a blend flow pipe via in-line mixing and the blended mixture is pumped through a single pipeline. In one or more embodiments, the in-line mixing system employs a separate spillback or recirculation loop that is fluidly connected to each set of the two or more sets of tanks to control the flow of the hydrocarbon fluid/liquid from each set of tanks to the blend flow pipe. Associated methods of operating one or more embodiments of the system include regulation of spillback or recirculation loop flow rate and/or pressure to drive the actual blend ratio towards a desired blend ratio.

First claim

Opening claim text (preview).

What is claimed is: 1. An in-line liquid mixing system to admix one or more of hydrocarbon liquids, petroleum liquids, or renewable liquids from a plurality of tanks into a single pipeline, the in-line liquid mixing system comprising: a first set of tanks, one or more tanks of the first set of tanks containing a first liquid of the one or more hydrocarbon liquids, petroleum liquids, or renewable liquids therein, each tank in the first set of tanks connected to and in liquid flow communication with a first header, thereby to transport a flow of the first liquid from the first set of tanks; a second set of tanks, one or more tanks containing a second liquid of the one or more hydrocarbon liquids, petroleum liquids, or renewable liquids therein, each tank in the second set of tanks connected to and in liquid flow communication with a second header, thereby to transport a flow of the second liquid from the second set of tanks; one or more first pumps each having an inlet and an outlet, the outlet of each of the one or more first pumps connected to one or more first booster pipes and the inlet of each of the one or more first pumps connected to the first header, thereby to increase pressure of liquid flow therethrough; one or more second pumps each having an inlet and an outlet, the outlet of each of the one or more second pumps connected to one or more second booster pipes and the inlet of the one or more second pumps connected to the second header, thereby to increase pressure of the liquid flow therethrough; one or more flow meters connected to one or more of: (a) the one or more first booster pipes, or (b) the one or more second booster pipes, thereby to measure a flow rate; one or more spillback pipes each having one or more control valves positioned to adjust a flow rate of liquid flow through the one or more spillback pipes between one or more of: (a) the one or more first booster pipes and the first header, or (b) the one or more second booster pipes and the second header; one or more blend pipes configured to admix liquid that flows from the one or more first booster pipes downstream of the one or more flow meters with liquid that flows through the one or more second booster pipes downstream, thereby to create a blend flow; and one or more blend meters connected to the one or more blend pipes, thereby to measure flow rate of the blend flow through the one or more blend pipes. 2. The in-line liquid mixing system of claim 1 , wherein the one or more spillback pipes comprise: (a) a first spillback pipe having a first connection to the one or more first booster pipes positioned between a first flow meter of the one or more flow meters and the one or more first pumps and a second connection to the first header upstream of the first set of tanks, the first spillback pipe including a first control valve of the one or more control valves, the first control valve configured to adjust a flow rate of liquid flow through the first spillback pipe between the one or more first booster pipes and the first header, and (b) a second spillback pipe having a first connection to the second booster pipe downstream of the second pump and a second connection to the second header upstream of the second set of tanks, the second spillback pipe including a second control valve of the one or more control valves, the second control valve configured to adjust a flow rate of liquid flow through the second spillback pipe between the one or more second booster pipes and the second header. 3. The in-line liquid mixing system of claim 2 , wherein the first spillback pipe includes a first differential pressure transmitter (DPIT) positioned to measure differential pressure of liquid flow upstream and downstream of the first control valve and the second spillback pipe includes a second DPIT positioned to measure differential pressure of liquid flow upstream and downstream of the second control valve. 4. The in-line liquid mixing system of claim 3 , further comprising one or more controllers in signal communication with each of the first control valve and the second control valve, and wherein the one or more controllers controls an open percentage of the first control valve to adjust the flow rate of the liquid flow through the first spillback pipe and thereby the first flow rate. 5. The in-line liquid mixing system of claim 4 , wherein the one or more controllers further is positioned in signal communication with the one or more flow meters, the first DPIT, and the second DPIT, wherein the one or more controllers determines the flow rate of liquid through the first spillback pipe based on the differential pressure measured by the first DPIT, and wherein the one or more controllers determines the flow rate of liquid through the second spillback pipe based on the differential pressure measured by the second DPIT. 6. The in-line liquid mixing system of claim 2 , further comprising one or more controllers in signal communication with each of the first control valve and the second control valve, and wherein the one or more controllers controls an open percentage of the first control valve to adjust the flow rate of the liquid flow through the first spillback pipe and thereby the first flow rate. 7. The in-line liquid mixing system of claim 2 , further comprising one or more controllers in signal communication with each of the first control valve and the second control valve, and wherein the one or more controllers controls an open percentage of the second control valve to adjust the flow rate of liquid flow through the second spillback pipe and thereby a ratio of first flow rate to blend liquid flow rate. 8. The in-line liquid mixing system of claim 2 , further comprising one or more controllers in signal communication with each of the first control valve and the second control valve, and wherein the one or more controllers adjusts the first control valve to drive the flow rate of the liquid flow through the first spill back pipe toward a first set point flow rate. 9. The in-line liquid mixing system of claim 8 , further comprising one or more controllers in signal communication with each of the first control valve and the second control valve, and wherein the one or more controllers adjusts the second control valve to drive the flow rate of the liquid flow through the first spill back pipe toward a second set point flow rate. 10. The in-line liquid mixing system of claim 2 , further comprising one or more controllers in signal communication with each of the first control valve and the second control valve, and wherein the one or more controllers adjusts at least one of the first control valve or the second control valve, thereby to drive a ratio of first flow rate to blend liquid flow rate toward a set point. 11. A method of admixing one or more hydrocarbon liquids, petroleum liquids, or renewable liquids from a plurality of sets of tanks into a single pipeline to provide in-line mixing thereof, the method comprising: initiating a blending process that includes blending two or more liquids of the one or more of the hydrocarbon liquids, petroleum liquids, or renewable liquids over a period of time, at least one of the two or more liquids being stored in a tank of a first set of tanks and at least another of the two or more liquids being stored in a tank of a second set of tanks, each tank of the first and second sets of tanks being connected to one or more blend pipes; thereby to blend the two or more liquids into a blended liquid; determining a density of each of the two or more liquids to be blended during the blending process; upon initiation of the blending process: determining a first flow rate of the one or more liquids flowing from the fir

Assignees

Inventors

Classifications

  • characterised by the disposition of the feed and discharge openings · CPC title

  • Flow control by valves, e.g. opening intermittently · CPC title

  • in which the mixture is discharged from and reintroduced into a receptacle through a recirculation tube, into which an additional component is introduced · CPC title

  • B01F23/49Primary

    Mixing systems, i.e. flow charts or diagrams · CPC title

  • G05D11/132Primary

    by controlling the flow of the individual components (G05D11/133 takes precedence) · CPC title

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What does patent US12011697B2 cover?
Methods and systems of admixing hydrocarbon liquids from two or more sets of tanks into a single pipeline to provide in-line mixing thereof. In an embodiment of the in-line mixing system, hydrocarbon liquids stored in at least one tank of each of two or more sets of tanks positioned at a tank farm are blended into a blend flow pipe via in-line mixing and the blended mixture is pumped through a …
Who is the assignee on this patent?
Marathon Petroleum Co Lp
What technology area does this patent fall under?
Primary CPC classification B01F23/49. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jun 18 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 12 related publications on this page (citations in our corpus or others sharing the same primary CPC).